CN100422230C - Method for producing core-shell high liquid-absorbing resin particle - Google Patents
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- CN100422230C CN100422230C CNB2005800013180A CN200580001318A CN100422230C CN 100422230 C CN100422230 C CN 100422230C CN B2005800013180 A CNB2005800013180 A CN B2005800013180A CN 200580001318 A CN200580001318 A CN 200580001318A CN 100422230 C CN100422230 C CN 100422230C
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- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F299/00—Macromolecular compounds obtained by interreacting polymers involving only carbon-to-carbon unsaturated bond reactions, in the absence of non-macromolecular monomers
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- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/22—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising organic material
- B01J20/26—Synthetic macromolecular compounds
- B01J20/261—Synthetic macromolecular compounds obtained by reactions only involving carbon to carbon unsaturated bonds
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- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/22—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising organic material
- B01J20/26—Synthetic macromolecular compounds
- B01J20/265—Synthetic macromolecular compounds modified or post-treated polymers
- B01J20/267—Cross-linked polymers
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- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/30—Processes for preparing, regenerating, or reactivating
- B01J20/32—Impregnating or coating ; Solid sorbent compositions obtained from processes involving impregnating or coating
- B01J20/3202—Impregnating or coating ; Solid sorbent compositions obtained from processes involving impregnating or coating characterised by the carrier, support or substrate used for impregnation or coating
- B01J20/3206—Organic carriers, supports or substrates
- B01J20/3208—Polymeric carriers, supports or substrates
- B01J20/321—Polymeric carriers, supports or substrates consisting of a polymer obtained by reactions involving only carbon to carbon unsaturated bonds
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- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/30—Processes for preparing, regenerating, or reactivating
- B01J20/32—Impregnating or coating ; Solid sorbent compositions obtained from processes involving impregnating or coating
- B01J20/3231—Impregnating or coating ; Solid sorbent compositions obtained from processes involving impregnating or coating characterised by the coating or impregnating layer
- B01J20/3242—Layers with a functional group, e.g. an affinity material, a ligand, a reactant or a complexing group
- B01J20/3268—Macromolecular compounds
- B01J20/327—Polymers obtained by reactions involving only carbon to carbon unsaturated bonds
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- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/30—Processes for preparing, regenerating, or reactivating
- B01J20/32—Impregnating or coating ; Solid sorbent compositions obtained from processes involving impregnating or coating
- B01J20/3291—Characterised by the shape of the carrier, the coating or the obtained coated product
- B01J20/3293—Coatings on a core, the core being particle or fiber shaped, e.g. encapsulated particles, coated fibers
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- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F265/00—Macromolecular compounds obtained by polymerising monomers on to polymers of unsaturated monocarboxylic acids or derivatives thereof as defined in group C08F20/00
- C08F265/02—Macromolecular compounds obtained by polymerising monomers on to polymers of unsaturated monocarboxylic acids or derivatives thereof as defined in group C08F20/00 on to polymers of acids, salts or anhydrides
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F265/00—Macromolecular compounds obtained by polymerising monomers on to polymers of unsaturated monocarboxylic acids or derivatives thereof as defined in group C08F20/00
- C08F265/04—Macromolecular compounds obtained by polymerising monomers on to polymers of unsaturated monocarboxylic acids or derivatives thereof as defined in group C08F20/00 on to polymers of esters
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- B—PERFORMING OPERATIONS; TRANSPORTING
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- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2220/00—Aspects relating to sorbent materials
- B01J2220/50—Aspects relating to the use of sorbent or filter aid materials
- B01J2220/68—Superabsorbents
Abstract
A method for producing a core-shell high liquid-absorbing resin particle is characterized by having (1) a first step for forming a particle core portion by suspension-polymerizing an aqueous solution (e) containing a (meth)acrylic acid, a crosslinking agent (c) and an anionic surfactant (d) in a hydrophobic organic solvent (a) containing a nonionic surfactant (b), and (2) a second step for forming a shell portion covering the particle core portion by suspension-polymerizing an aqueous solution (g) containing a water-soluble vinyl polymer (f) with a number-average molecular weight of 500-10,000 having a carboxyl group and a polymerizable unsaturated double bond in the suspension obtained in the first step.
Description
Technical field
The present invention relates to be applicable to the various fields headed by medical treatment, the health field, according to the manufacture method of the high liquid-absorbing resin particle of the anti-phase suspension polymerization of water-in-oil-type.
Background technology
The absorbency resin can absorb the water of its quality several times and blood etc., is applicable to and sanitary product and diaper etc. is applicable to water repellent agent etc. with regard to building field with regard to medical treatment, health field.
Wherein, for the absorbency resin that is used for sanitary product and diaper, as the high added value commodity, requirement absorbing blood and urine fully also can be because of leakage pollution clothes class etc.Want to prevent the seepage of blood in the sanitary product etc. etc., not only to improve the absorbency of absorbency resin, and importantly under equally distributed state, keep the absorbency resin in cartridge inside such as sanitary products, carried out various researchs in order to improve these problems.Wherein so-called cartridge be constitute sanitary product and diaper a part can absorbing blood and the position of urine, the part etc. of the mixture of cotton-shaped fibre stuff and emboliform absorbency resin being wrapped formation with non-woven fabrics etc. is for example arranged.
In recent years, from its degree easy to manufacture, studied with so-called water-in-oil-type anti-phase suspension polymerization and made the absorbency resin, wherein said water-in-oil-type anti-phase suspension polymerization is that dropping contains the aqueous solution of free-radical polymerised compound and polymerization starter and stirs in organic solvent, make its little being scattered in the organic solvent, thereby in the water droplet that obtains, make free-radical polymerised compound carry out polymerization.But, the absorbency resin that obtains with above-mentioned manufacture method since usually the surface be level and smooth granular, so be difficult at the cartridge internal load on cotton-shaped fibre stuff, thereby be easy to produce biasing aspect its distribution.This result, such cartridge is absorbing blood etc. fully, is easy to cause seepage.In addition, the absorbency resin that is obtained by above-mentioned manufacture method is very little owing to its particle diameter, thus need dust disposal measure etc., and then aspect operability, also have problems.
As the method that addresses this problem, reported with suspension polymerization can make the resin stationarity big, promptly be difficult at the inner super absorbent resin that produces biasing of cartridge, wherein said suspension polymerization is to supply with one by one in the hydrophobic organic solvent that contains nonionic class dispersion agent by containing the aqueous solution (for example, referring to Patent Document 1) that special phosphate class dispersion agent and water-soluble ethylene monomer form.
But above-mentioned super absorbent resin is not enough to the affinity of blood and urine etc., and is when as sanitary product etc., not talkative fully with regard to the viewpoint of absorbency, especially sucking blood property.In addition, above-mentioned super absorbent resin has the problem that so-called absorbency significantly descends when multiple absorption blood etc.
In addition, reported that the absorbent resin that obtains with the following method has than with the especially excellent absorption characteristic to blood of contact: in the inert solvent that contains special phosphate class tensio-active agent, supply with the aqueous solution that contains above-mentioned phosphoric acid ester tensio-active agent, specific poly-acidic amino acid, alkene unsaturated compound and linking agent, make its suspension polymerization, thus obtained polymer particle is carried out surface-crosslinked processing (for example, referring to Patent Document 2).
But, though there is so-called problem with tone of brown class in sucking blood property of the absorbent resin excellence of using poly aspartic acid to obtain as above-mentioned specific poly-acidic amino acid.
Medical treatment, the health field that utilizes the sanitary product of absorbency resin and diaper etc. is the field of special cleaning of requirement and health, above-mentioned absorbency resin presents the tone of brown class owing to given antihygienic impression of infringement clean feel, be fatal defective as much as to say, thereby the utility value on the industry in this field significantly descend.
Patent documentation 1: the spy opens the 2001-31704 communique
Patent documentation 2: the spy opens the 2003-206324 communique
Summary of the invention
Yan Jiukaifa result has up to now improved the absorbency of absorbency resin as mentioned above significantly.But, though to keeping high-caliber absorbency, particularly sucking blood property etc., and tone with clean feel, hope is white, also go for the positive sharp increase of demand of the super liquid-absorbent resin of medical treatment, health field, also be not developed but present case is the super liquid-absorbent resin that satisfies aforesaid requirement.
The problem that the present invention wants to solve provides absorbency, sucking blood property excellence especially, even make its multiple absorption blood also can keep the manufacture method of the core-shell high liquid-absorbing resin particle of excellent certain tone sucking blood property, that have clean feel.
The inventor etc. are in order to solve above-mentioned problem, be conceived to the sucking blood property of the excellence that resin particle had that obtains with above-mentioned suspension polymerization in the past, with improve its tone, further seek sucking blood property, the level that especially repeats sucking blood property rises to policy research.
At first make hydrophobic organic solvent contain nonionic surfactant, in the above-mentioned hydrophobic organic solvent that keeps polymeric reaction temperature, make the aqueous solution that contains (methyl) vinylformic acid, linking agent and anionic surfactant carry out suspension polymerization, thereby as the absorbency resin is excellent shapes such as operability, and has obtained to have the particles of acrylic polymer of the suitable particle diameter of hundreds of μ m.But, though this particles of acrylic polymer has sucking blood property to a certain degree, sucking blood property decline when making it repeat to suck blood, it is still not enough to repeat sucking blood property.
Therefore, carried out research further, results verification makes the aqueous solution that contains above-mentioned (methyl) vinylformic acid etc. carry out suspension polymerization in above-mentioned hydrophobic organic solvent, when this polyreaction has been carried out to a certain degree, have carboxyl and polymerizability unsaturated double-bond by making to contain again, and the tone that the aqueous solution of water-soluble ethylene based polyalcohol with number-average molecular weight of specified range carries out the core-shell high liquid-absorbing resin particle that suspension polymerization obtains is the white with clean feel, its sucking blood property and to repeat sucking blood property also fabulous has so far been finished the present invention in addition.
Promptly, the invention provides the manufacture method of core-shell high liquid-absorbing resin particle, it is characterized in that having (1) in the hydrophobic organic solvent that contains nonionic surfactant (b) (a), make the aqueous solution (e) that contains (methyl) vinylformic acid, linking agent (c) and anionic surfactant (d) carry out suspension polymerization and form the particle core first operation and
(2) in the suspension that obtains by above-mentioned first operation, make to contain to have carboxyl and polymerizability unsaturated double-bond, and the aqueous solution (g) with water-soluble ethylene based polyalcohol (f) of 500～10000 number-average molecular weights carries out suspension polymerization and forms second operation of the shell portion that covers above-mentioned particle core.
The invention effect
According to the present invention, can provide absorbency, sucking blood property excellence especially, even its sucking blood property of multiple absorption blood also can not descended and can keep the manufacture method of the core-shell high liquid-absorbing resin particle of excellent white sucking blood property, that have clean feel.
The core-shell high liquid-absorbing resin particle that obtains according to manufacture method of the present invention for example is suitable for sanitary towel, cotton balls, medical blood absorbing sheet, the absorption agent that drips, wound protecting materials, wound healing material, operation most with medical treatment, sanitary use such as waste liquor treating agents.In addition, above-mentioned super liquid-absorbent resin is except being used for blood, owing to for example absorptivity excellence of urine, seawater, cement, the soil water, the water that contains fertilizer, rainwater, draining etc., so also be applicable to civil construction purposes such as hydroexpansivity rubber, water repellent agent.
Description of drawings
[Fig. 1] is the photo that uses scanning electron microscope to take according to multiplying power 200 to the high liquid-absorbing resin particle (A) that is obtained by embodiment 1.
[Fig. 2] is the photo that uses scanning electron microscope to take according to multiplying power 500 to the high liquid-absorbing resin particle (A) that is obtained by embodiment 1.
Embodiment
The present invention relates to make its suspension polymerization make the method for core-shell high liquid-absorbing resin particle by in hydrophobic organic solvent, supplying with the aqueous solution that contains free-radical polymerised compound.
Above-mentioned suspension polymerization is carried out according to two step operations.That is, modulate two kinds of aqueous solution that contain free-radical polymerised compound etc. in advance, respectively each aqueous solution is supplied with in hydrophobic organic solvent, thereby adopt the operation of carrying out suspension polymerization according to two steps.
In first operation, by in the hydrophobic organic solvent that contains nonionic surfactant (b) (a) that keeps polymeric reaction temperature, supply with and contain (methyl) vinylformic acid, linking agent (c) and anionic surfactant's (d) the aqueous solution (e) and make it carry out suspension polymerization to form the particle core.
In second operation, by in the suspension that obtains by above-mentioned first operation, supply contains and has carboxyl and polymerizability unsaturated double-bond, and have 500～10000 number-average molecular weights water-soluble ethylene based polyalcohol (f) the aqueous solution (g) and make it carry out suspension polymerization to form the shell portion that covers above-mentioned particle core.
As the method for in above-mentioned first operation, supplying with the aqueous solution (e), preferably not disposable, but supply with the aqueous solution (e) one by one, promptly supply with in right amount through the time to a certain degree discontinuously or continuously.By supplying with the aqueous solution (e) one by one, can the aqueous solution (e) be separated under the tiny drop-shaped state and carry out Raolical polymerizable, and can obtain to have pulverous particles of acrylic polymer of desirable particle diameter as described later.The conditions such as the feed rate of the aqueous solution (e) and time of supplying with are one by one preferably suitably set according to conditions such as the whipped state of hydrophobic organic solvent (a) and reaction scale, so that in hydrophobic organic solvent (a) aqueous solution (e) is remained as the dispersed state of tiny water droplet.
Need remain on that the free-radical polymerised compound that contains for the aqueous solution (e) that makes supply and the aqueous solution (g) carries out polyreaction to hydrophobic organic solvent (a) and in the temperature range of needs.The difference of the kind of this temperature range operable radical polymerization initiator during etc. and difference according to above-mentioned Raolical polymerizable, but preferred in 40～150 ℃ scope, more preferably in 60～90 ℃ scope.
The above-mentioned aqueous solution of supplying with in above-mentioned first operation (e) disperses with tiny drops in hydrophobic organic solvent (a), and (methyl) vinylformic acid and the linking agent free-radical polymerised compounds such as (c) that contain at this water droplet directly carry out suspension polymerization.That is, supply with one by one the aqueous solution (e) during also carry out polyreaction, form particles of acrylic polymer.
The aqueous solution of preferably supplying with in above-mentioned second operation (g) is after supplying with the above-mentioned aqueous solution (e) end, the whole polyreaction of (methyl) vinylformic acid that in the aqueous solution (e), contains and linking agent (c) before finishing fully during, promptly roughly just finished back～2 hours with interior supply supplying with the aqueous solution (e).So, particles of acrylic polymer that forms in above-mentioned first operation and above-mentioned water-soluble ethylene based polyalcohol (f) can form chemically combined resin particle, final sucking blood property of the core-shell high liquid-absorbing resin particle excellence that obtains also is difficult to descend even make it repeat sucking blood property.
The supply of the aqueous solution (g) also can be disposable supply and supply with one by one any one.
As mentioned above, the free-radical polymerised compound that is contained in the above-mentioned aqueous solution (e) that the hydrophobic organic solvent (a) in remaining on the temperature range that needs in order to carry out polyreaction is supplied with in first operation carries out polyreaction immediately.Therefore, when in second operation, supplying with the aqueous solution (g), consider that the great majority of this free-radical polymerised compound have been finished polyreaction, promptly form the particle core.Therefore, the major part of the water-soluble ethylene based polyalcohol of supplying with in second operation (f) forms shell portion according to the mode that this particle core that will form surrounds, and the high liquid-absorbing resin particle that this result obtains has so-called core-shell structure.
Among the present invention, make hydrophobic organic solvent (a) contain nonionic surfactant (b), use anionic surfactant (d) in this external aqueous solution (e).The using method of these two kinds of tensio-active agents also is important with regard to can obtaining effect of the present invention.
That is, though in the present invention according to making the aqueous solution (e) carry out suspension polymerization with the state that tiny drops is scattered in the hydrophobic organic solvent (a), the polymer particle that carries out forming in the process in polyreaction condenses to a certain extent.If should the cohesion degree little, then can not realize effect of the present invention fully, must avoid excessive cohesion simultaneously certainly in addition.
By adopting the method for above-mentioned use tensio-active agent, though detailed reason and unclear, the cohesion degree of this polymer particle is controlled to be made as suitable state, and the surface of polymer particle has significantly concavo-convex.This result is that can to obtain sucking blood property excellent especially, also is difficult to the core-shell high liquid-absorbing resin particle that descends even make it repeat sucking blood property.
Want to carry out well the anti-phase suspension polymerization of water-in-oil-type among the present invention, importantly when supplying with the aqueous solution (e) and the aqueous solution (g), fully stir hydrophobic organic solvent (a).This agitation condition is according to the kind of the agitator that uses, the differences such as size of reactor.For example have dividing plate, possessing the 1m of common anchor stirrer when imaginary
3When stirring in the reactor, the rotation number of preferred agitator is in the scope of 40～100rpm, more preferably in the scope of 50～90rpm.
After hydrophobic organic solvent (a) is supplied with the aqueous solution (g), for example, stirred 10 minutes～3 hours down in above-mentioned second operation, can obtain to contain the pulp-like mixture of the high liquid-absorbing resin particle of swelling at 60～80 ℃.The high liquid-absorbing resin particle that obtains for example can be with azeotropic dehydration and heat drying method etc., with the mixture separation of above-mentioned pulp-like.
Above-mentioned azeotropic dehydration be with the mixture of above-mentioned pulp-like with the azeotropic temperature of water and hydrophobic organic solvent (a) under the heating certain hour carry out dehydration method.Use above-mentioned azeotropic dehydration, after the water dehydration with 75～95 quality % that contain in the above-mentioned pulp-like mixture, can with filtration method high liquid-absorbing resin particle be separated with hydrophobic organic solvent (a) with for example decantation, and make its drying, thereby obtain pulverous core-shell high liquid-absorbing resin particle.
Above-mentioned heat drying method for example is to use Vacuumdrier, warm braw drying machine, pneumatic drier, fluid bed dryer, rotary dryer etc. to make water and hydrophobic organic solvent (a) evaporation, thereby obtains the method for pulverous core-shell high liquid-absorbing resin particle.Drying temperature is preferably more than 50 ℃, in more preferably 60 ℃～200 ℃ the scope, in further preferred 70 ℃～180 ℃ scope.By in this temperature range, making its drying, can prevent that the absorbency that the thermolysis because of high liquid-absorbing resin particle causes from descending.
The core-shell high liquid-absorbing resin particle that is obtained by manufacture method of the present invention preferably has the median size in 100 μ m～1000 mu m ranges, more preferably has the median size in 100 μ m～500 mu m ranges.High liquid-absorbing resin particle with the median size in this scope is difficult to up waft in its manufacturing processed, does not need the dust disposal measure.
Above-mentioned median size is that high liquid-absorbing resin particle is carried out classification with a plurality of sieves, by high liquid-absorbing resin particle residual on each sieve, make size distribution, the value the when aggregate-value of above-mentioned sieve lingering section is 50 quality % in this size distribution with respect to the size of the aggregate-value of the mass ratio that is used for fractionated high liquid-absorbing resin particle total amount (sieve lingering section) and each sieve corresponding with it.
Below, the various raw materials that use in the manufacture method to core-shell high liquid-absorbing resin particle of the present invention are described in detail.
As the hydrophobic organic solvent that uses among the present invention (a), can use for example aliphatic hydrocarbon solvents such as Skellysolve A, normal hexane, normal heptane, octane; Clicyclic hydrocarbon such as hexanaphthene, methylcyclohexane solvent; Aromatic hydrocarbon solvents such as benzene,toluene,xylene etc., wherein preferred normal hexane, normal heptane, hexanaphthene.
Above-mentioned hydrophobic organic solvent (a) preferably uses 0.5～10 times with respect to above-mentioned (methyl) the acrylic acid quality that contains in the above-mentioned aqueous solution (e), more preferably uses 0.8～3 times.Above-mentioned hydrophobic organic solvent (a) if usage quantity in above-mentioned scope, then can suppress the excessive cohesion of core-shell high liquid-absorbing resin particle, prevent that absorbency from descending.
Below, the nonionic surfactant (b) that uses among the present invention is described.
As above-mentioned nonionic surfactant (b), can enumerate for example polyoxyalkylene fatty acid ester such as polyoxyalkylene sorbitan fatty(acid)ester, polyoxyalkylene Sorbitol Powder fatty acid ester, polyoxyalkylene glycerol fatty acid ester and sorbitan fatty(acid)ester, sucrose fatty ester, glycerol fatty acid ester, polyoxyalkylene alkyl, phosphotriester, polyoxyethylene polyoxypropylene block copolymers etc., these can use separately, perhaps also can more than two kinds and use.
As above-mentioned polyoxyalkylene sorbitan fatty(acid)ester, can use for example polyoxyethylene anhydrosorbitol monostearate, polyoxyethylene anhydrosorbitol tristearate, polyoxyethylene dehydrating sorbitol monooleate, polyoxyethylene anhydrosorbitol trioleate etc.
As above-mentioned sorbitan fatty(acid)ester, can use for example Span 20, anhydrosorbitol monostearate, anhydrosorbitol tristearate, dehydrating sorbitol monooleate, anhydrosorbitol trioleate etc.
As above-mentioned sucrose fatty ester, can use for example sucrose stearate, Surfhope SE Cosme C 1616, Sugar Ester O 1570, Surfhope SE Cosme C 1216 etc.
As above-mentioned polyoxyalkylene Sorbitol Powder fatty acid ester, can use for example polyoxyethylene Sorbitol Powder four oleic acid esters etc.
As above-mentioned polyoxyalkylene glycerol fatty acid ester, can use for example polyoxyethylene glycerol monostearate, polyoxyethylene glycerol monoleate etc.
As above-mentioned glycerol fatty acid ester, can use for example Zerol, glyceryl monooleate, Monooctamoin etc.
As above-mentioned polyoxyalkylene alkyl, can use for example polyoxyethylene lauryl ether, polyoxyethylene cetyl ether, polyoxyethylene stearyl-ether etc.
As above-mentioned phosphotriester, can use for example polyethylene oxide alkyl ethers phosphoric acid etc.
The influence of the particle shape of the core-shell high liquid-absorbing resin particle that structure that above-mentioned nonionic surfactant (b) has and wetting ability-lipophilicity balance (hereinafter referred to as " HLB ") obtains can be observed out some relations between the absorbency that its particle shape and this high liquid-absorbing resin particle have.Above-mentioned in addition HLB is usually as the wetting ability of presentation surface promoting agent and the yardstick (JIS K3211) of lipophilicity degree.
In above-mentioned nonionic surfactant (b), has the roughly nonionic surfactant of the HLB of 4～13 scopes if use, then can obtain particle surface and have obvious concavo-convex high liquid-absorbing resin particle, thereby the absorbency that can judge this high liquid-absorbing resin particle is excellent especially.In addition, have specific structure if use, and have the nonionic surfactant of being shown in of specific HLB following (1)～(3), then owing to having shown the effect that improves absorbency more significantly, so preferred.
(1) has the polyoxyalkylene sorbitan fatty(acid)ester of 9～11HLB.
(2) has the polyoxyalkylene glycerol fatty acid ester of 9～10HLB.
(3) has the phosphotriester of 7～13HLB.
Above-mentioned nonionic surfactant (b) preferably uses in 0.01～5 quality % scope with respect to above-mentioned hydrophobic organic solvent (a).Above-mentioned nonionic surfactant (b) if usage quantity in above-mentioned scope, the particle core of being made up of the aforesaid propylene acid polymer that is obtained by first operation is well-dispersed in the above-mentioned hydrophobic organic solvent (a).
; the acrylate copolymer that forms core-shell high liquid-absorbing resin particle constructed in accordance is to be the polymkeric substance of the free-radical polymerised compound of principal constituent with (methyl) vinylformic acid; but except above-mentioned (methyl) vinylformic acid, can also use can with other vinyl monomer of its copolymerization.
As above-mentioned other vinyl monomer, can in the scope of not damaging the effect that obtains according to the present invention, use acrylamide-2-methyl propane sulfonic acid, sulfonic acid allyl ester, vinyl sulfonic acid, methacrylic acid 4-thiosulfate pentahydrate and (methyl) acrylamide, N, N-DMAA, N-methylol (methyl) acrylamide, (methyl) vinylformic acid 2-hydroxyl ethyl ester etc., wherein preferred (methyl) acrylamide.
Above-mentioned other vinyl monomer can be in the scope that with respect to above-mentioned (methyl) vinylformic acid 100 mass parts is 0～100 mass parts and is used.But, in order to obtain sucking blood property excellence, even and make it repeat sucking blood property also to be difficult to the high liquid-absorbing resin particle that descends, preferably in the scope of 0～5 mass parts and with above-mentioned other vinyl monomer, more preferably use (methyl) vinylformic acid separately only.
The carboxyl that above-mentioned (methyl) vinylformic acid has preferably neutralizes with basic cpd, and when above-mentioned other vinyl monomer had carboxyl or alkylsulfonyl, preferably these also neutralized with basic cpd in addition.20～100 moles of % of preferred above-mentioned carboxyl or alkylsulfonyl are neutralized, and more preferably 30～60 moles of % are neutralized.By with carboxyl in the above-mentioned scope or alkylsulfonyl neutralization, can improve the absorbency of the high liquid-absorbing resin particle of acquisition.
As above-mentioned basic cpd, can use for example sodium hydroxide, potassium hydroxide, lithium hydroxide, rubidium hydroxide etc., wherein preferred sodium hydroxide and potassium hydroxide.
Below, the linking agent (c) that uses among the present invention is described.
As operable linking agent (c) among the present invention, can enumerate monomer (cI) that for example has free-radical polymerised unsaturated double-bond more than two or compound (cII) with the functional group who reacts with carboxyl more than two.By using above-mentioned monomer (cI) or above-claimed cpd (cII), can obtain absorbency, the super liquid-absorbent resin of sucking blood property excellence especially.
As above-mentioned monomer (cI), can use for example two (methyl) acrylate, three (methyl) acrylate, bisacrylamide, multivalence allylic cpd etc. with free-radical polymerised unsaturated double-bond more than two.
As above-mentioned two (methyl) acrylate, can use for example two (methyl) vinylformic acid glycol ester, two (methyl) vinylformic acid propylene glycol ester, two (methyl) polyalkylene glycol acrylate ester, two (methyl) vinylformic acid polypropylene glycol ester, formamyl two (methyl) acrylate etc.
As above-mentioned three (methyl) acrylate, can use for example trimethylolpropane tris (methyl) acrylate, tetramethylolmethane three (methyl) acrylate etc.
As above-mentioned bisacrylamide, can use for example N, N '-methylene-bisacrylamide, N, N '-ethylenebis acrylamide etc.
As above-mentioned multivalence allylic cpd, can use for example diallyl phthalate, tetraallyl oxygen base ethane, tetramethylolmethane three allyl ethers, trimethylolpropane tris allyl ether, Diethylene Glycol diallyl ether, triphen pregnancy acid triallyl etc.
In above-mentioned monomer (cI), also preferably use two (methyl) vinylformic acid glycol ester, two (methyl) vinylformic acid propylene glycol ester, two (methyl) polyalkylene glycol acrylate ester, N, N '-methylene-bisacrylamide, by using these, can obtain absorbency, the high liquid-absorbing resin particle of sucking blood property excellence especially.
As above-mentioned compound (cII), can use the compound that for example has two above epoxy group(ing), compound etc. with two above isocyanate group with the functional group who reacts with carboxyl more than two.
As above-mentioned compound with two above epoxy group(ing), can use for example ethylene glycol diglycidylether, polyethyleneglycol diglycidylether, propylene glycol diglycidylether, polypropylene glycol diglycidyl ether, glycerin diglycidyl ether, Polyglycerine diglycidylether etc., wherein preferred ethylene glycol diglycidylether.
As above-mentioned compound, can use various polymeric polyisocyanates with water dispersible with two above isocyanate group.
Above-mentioned linking agent (c) preferably uses in the scope that with respect to above-mentioned (methyl) vinylformic acid 100 mass parts is 0.01～1 mass parts.Above-mentioned linking agent (c) if usage quantity less than 0.01 mass parts, then the internal crosslinking of the core-shell high liquid-absorbing resin particle of Huo Deing becomes not enough, the stability decreases of absorbency when repeating imbibition and the liquid that kept absorbing.In addition, above-mentioned linking agent (c) then owing to the high liquid-absorbing resin particle that causes acquisition sometimes excessively condenses, reduces absorbency, so not preferred if surpass 1 mass parts.The usage quantity of above-mentioned linking agent (c) is in the scope of 0.01～0.5 mass parts with respect to above-mentioned (methyl) vinylformic acid 100 mass parts more preferably.
Below, the anionic surfactant (d) who uses among the present invention is described.
As above-mentioned anionic surfactant (d), can use for example N-acyl amino hydrochlorate, polyethylene oxide alkyl ethers carboxylate salt, acylated peptide, alkylsulfonate, alkylbenzene sulfonate, sulfonated alkyl naphathalene, naphthalenesulfonate-formalin polycondensate, thio succinate, sulfonated, N-acyl group sulfonate, polyethylene oxide alkyl ethers sulfonate, alkylamide vitriol, alkylphosphonic, polyethylene oxide alkyl ethers phosphate ester salt, polyoxyethylene allylic alkylation allyl ethers phosphate ester salt, sulfonation wet goods.
In above-mentioned anionic surfactant (d), the also preferred sulfonate that uses following with general formula (I) expression.By using following sulfonate, can suppress to stick on the wall and agitator of reactor by the particles of acrylic polymer that above-mentioned first operation obtains with general formula (I) expression.
R’-SO
3M (I)
R ' expression in the above-mentioned general formula (I) has the alkenyl of carbonatoms 8～30 or has the hydroxyalkyl of carbonatoms 8～24.M represents basic metal, quaternary ammonium salt or quaternary ammonium.
As above-mentioned alkenyl, can enumerate for example cetene base, tetradecene base, dodecenyl succinic, vaccenic acid base, decene base, octenyl etc. with carbonatoms 8～30.
As above-mentioned sulfonate, can use for example vaccenic acid sodium sulfonate, cetene sodium sulfonate, tetradecene sodium sulfonate, dodecylene sodium sulfonate, decene sodium sulfonate, octene sodium sulfonate etc. with alkenyl of carbonatoms 8～30.
As above-mentioned hydroxyalkyl, can enumerate for example hydroxyl lauryl, hydroxyl octyl group, hydroxyl hexadecyl, hydroxyl tetradecyl, hydroxyl octadecyl, hydroxyl decyl etc. with carbonatoms 8～24.
As above-mentioned sulfonate, can use for example hydroxyl sodium laurylsulfonate, hydroxyl sodium octyl, hydroxyl sodium cetanesulfonate, hydroxyl tetradecyl sodium sulfonate, hydroxyl octadecyl sodium sulfonate, hydroxyl decyl sodium sulfonate etc. with hydroxyalkyl of carbonatoms 8～24.
In addition, as above-mentioned anionic surfactant (d), can use the sulfonate of the sulfonate of above-mentioned alkenyl with carbonatoms 8～30 and above-mentioned hydroxyalkyl with carbonatoms 8～24 mixture, be sulfonated.
Above-mentioned anionic surfactant (d) preferably uses in the scope that with respect to above-mentioned (methyl) vinylformic acid 100 mass parts is 1～10 mass parts.Above-mentioned anionic surfactant's (d) usage quantity is if in this scope, then can be under the state that is fit to the extent control of aforesaid propylene acid polymer particle coacervation, thus can obtain to have the core-shell high liquid-absorbing resin particle of tangible concavo-convex absorbency excellence at particle surface.
Below operable radical polymerization initiator among the present invention is described.
Among the present invention, carry out Raolical polymerizable, can use radical polymerization initiator in order to make (methyl) vinylformic acid and the above-mentioned linking agent (c) that are contained in the above-mentioned aqueous solution (e) that in first operation, use.As above-mentioned radical polymerization initiator, can enumerate for example superoxide such as hydrogen peroxide, Potassium Persulphate, Sodium Persulfate, ammonium persulphate, with 2,2 '-azo is two-(amino two propane of 2-) dihydrochloride, 2, and 2 '-azo is two-(N, N '-dimethylene isobutyl amidine) dihydrochloride, 2,2 '-azo is two-{ 2-methyl-N-[1, two (the methylol)-2-hydroxyethyls of 1-] propionic acid amide } wait azo-compound, these can use separately, perhaps also can be more than two kinds and usefulness.Above-mentioned superoxide can use simultaneously with reducing substances such as phosphite, L-xitix and amine salt etc., can be as the initiator of redox system.
Above-mentioned radical polymerization initiator preferably uses in the scope that with respect to above-mentioned (methyl) vinylformic acid 100 mass parts is 0.1～1 mass parts.If the usage quantity of above-mentioned radical polymerization initiator in above-mentioned scope, then can be adjusted into suitable scope according to the mode of the core-shell high liquid-absorbing resin particle of making the absorbency excellence with the molecular weight of the aforesaid propylene acid polymer particle that obtains.
Above-mentioned (methyl) vinylformic acid, above-mentioned linking agent (c) and above-mentioned anionic surfactant (d) supply in the above-mentioned hydrophobic organic solvent (a) one by one as the aqueous solution (e).The above-mentioned aqueous solution (e) can be by mixing above-mentioned (methyl) vinylformic acid, above-mentioned linking agent (c) and above-mentioned anionic surfactant (d), as required above-mentioned other vinyl monomer and radical polymerization initiator to stir and make with water.
Below, have carboxyl and a polymerizability unsaturated double-bond to what use among the present invention, and the aqueous solution (g) with water-soluble ethylene based polyalcohol (f) of 500～10000 number-average molecular weights describes.
The carboxyl that water-soluble ethylene based polyalcohol (f) is had also can neutralize with basic cpd.As this basic cpd, can use with as in (methyl) carboxyl that vinylformic acid had that can be used for containing at the above-mentioned aqueous solution (g) and the time the identical material enumerated of material.
In addition, water-soluble ethylene based polyalcohol (f) preferably has the acid number in 130～800 scopes, more preferably has the acid number in 300～500 scopes.Have the water-soluble ethylene based polyalcohol (f) of the acid number in this scope by use, can improve the sucking blood property of core-shell high liquid-absorbing resin particle of acquisition and the maintenance stability of blood, the decline of sucking blood property in the time of can suppressing to make the blood multiple absorption.
Preferably there is 1～3 in the polymerizability unsaturated double-bond that water-soluble ethylene based polyalcohol (f) is had in a part water-soluble ethylene based polyalcohol (f).Have the water-soluble ethylene based polyalcohol (f) of the polymerizability unsaturated double-bond in this scope by use, the core-shell high liquid-absorbing resin particle that can suppress to obtain excessively condenses, and can prevent the decline of sucking blood property.
The variation of sucking blood property when the number-average molecular weight influence that water-soluble ethylene based polyalcohol (f) is had makes the core-shell high liquid-absorbing resin particle of acquisition repeat to suck blood.Even also can keep the viewpoint of the sucking blood property of excellence from multiple absorption blood, the number-average molecular weight that water-soluble ethylene based polyalcohol (f) is had is preferably in 500～10000 the scope, more preferably in 1000～5000 the scope, further in preferred 2000～4000 the scope.
Water-soluble ethylene based polyalcohol (f) for example can be made by the vinyl polymer with carboxyl is reacted in water with the compound with epoxy group(ing) and polymerizability unsaturated double-bond.
Above-mentioned vinyl polymer with carboxyl can be the Lustrex that a kind of polymerization of vinyl monomer is obtained, and also can be segmented copolymer or the random copolymers that the polymerization of vinyl monomer more than two kinds is obtained.
Above-mentioned vinyl polymer with carboxyl for example can carry out the incompatible manufacturing of radical polymerization by making vinyl monomer and other vinyl monomer as required with carboxyl in the presence of radical polymerization initiator and water.
As above-mentioned vinyl monomer with carboxyl, for example can use (methyl) vinylformic acid, toxilic acid, fumaric acid etc., wherein preferably use (methyl) vinylformic acid.
As above-mentioned other vinyl monomer, for example can use (methyl) acrylamide, (methyl) vinylformic acid 2-hydroxyl ethyl ester, (methyl) vinylformic acid 2-hydroxypropyl acrylate, (methyl) vinylformic acid 2-hydroxy butyl ester etc. to have the vinyl monomer of amide group or hydroxyl.Be used in combination even will have vinyl monomer and above-mentioned (methyl) vinylformic acid of amide group or hydroxyl, also be difficult to reduce the sucking blood property of the core-shell high liquid-absorbing resin particle of acquisition.
As above-mentioned vinyl monomer with carboxyl, can use vinylformic acid to carry out the polyacrylic acid that polymerization obtains, but preferred mode according to the high liquid-absorbing resin particle of making the absorbency excellence.
As above-mentioned radical polymerization initiator, can use and the conduct identical material of radical polymerization initiator that operable as required material is enumerated in above-mentioned first operation.
As with the compound with epoxy group(ing) and polymerizability unsaturated double-bond of above-mentioned vinyl polymer reaction with carboxyl, can use for example allyl glycidyl ether, (methyl) glycidyl acrylate etc.Wherein, also preferred (methyl) glycidyl acrylate that uses is because can suppress and the above-mentioned side reaction of vinyl polymer in water with carboxyl.
The usage quantity of water-soluble ethylene based polyalcohol (f) is the scope of 3～10 mass parts with respect to above-mentioned (methyl) vinylformic acid 100 mass parts preferably in the manufacture method of the present invention.That is, be preferably in the aqueous solution (g) that uses the water-soluble ethylene based polyalcohol (f) that contains above-mentioned usage quantity in above-mentioned second operation.The usage quantity of water-soluble ethylene based polyalcohol (f) is if in this scope, and then the core-shell high liquid-absorbing resin particle of Huo Deing has excellent absorbency, especially excellent the sucking blood property characteristic that repeats.
In above-mentioned second operation in the manufacture method of high liquid-absorbing resin particle of the present invention, can in the scope of not damaging the object of the invention, use for example to make alginic acid and hyaluronic acid etc. have the high-molecular weight compound of hydroxyl and carboxyl and the aqueous solution of the compound that above-mentioned compound reaction with epoxy group(ing) and polymerizability unsaturated double-bond obtains with the aqueous solution (g) of above-mentioned water-soluble ethylene based polyalcohol (f) with polymerizability unsaturated double-bond and carboxyl.
Embodiment
Below, show embodiments of the invention.
In addition, the sucking blood property shown in the table 1 and repeat the evaluation of sucking blood property and the measurement of median size and number-average molecular weight is carried out with the method shown in following.
[evaluation method of sucking blood property]
Among the high liquid-absorbing resin particle 1g in the basin of internal diameter 95mm, add defibrinated horse blood (Co., Ltd. Japan biomaterial center system) 20g, it was sucked blood 1 minute.After 1 minute,, thereby remove the remaining blood of not sucked blood at the high liquid-absorbing resin particle of placing on the filter paper of the 20cm diameter that 5 are piled up after sucking blood.Deduct the quality of the high liquid-absorbing resin particle before sucking blood by the quality of the high liquid-absorbing resin particle after sucking blood, obtain the amount of sucking blood (g) of every 1g high liquid-absorbing resin particle.
[repeating the evaluation method of sucking blood property]
Add defibrinated horse blood 2.5g among the high liquid-absorbing resin particle 0.5g in the basin of internal diameter 95mm, measure up to the time that absorbs defibrinated horse blood fully.Add after the defibrinated horse blood through after 2 minutes, add defibrinated horse blood 2.5g again, measure up to the time that absorbs defibrinated horse blood fully.
[measuring method of median size]
16 purpose sieves, 30 purpose sieves, 100 purpose sieves, 140 purpose sieves and 235 purpose sieves and the take-up reel of satisfying the specification of putting down in writing among the JIS Z8801-1 are made up in order from top, in 16 purpose sieves of topmost, add high liquid-absorbing resin particle 20g, fully vibration.After the vibration, obtain the mass ratio (sieve lingering section) of high liquid-absorbing resin particle residual on each sieve with respect to the high liquid-absorbing resin particle total amount.Size by value that begins from the big side of sieve mesh the accumulation of each sieve lingering section is formed and the sieve mesh corresponding with it is made size distribution, and the size of sieve mesh is defined as median size when above-mentioned value with each sieve lingering section accumulation formation is 50 quality % in this size distribution.
[measuring method of number-average molecular weight]
Use has post (eastern ソ-Co., Ltd.'s system, TSKGEL G5000PWXL) and post (eastern ソ-Co., Ltd.'s system, TSKGEL G3000PWXL) joint pin, detector (eastern ソ-Co., Ltd.'s system, RI-8000) and pump (eastern ソ-Co., Ltd.'s system, CCPM) liquid chromatograph, (pH=0.7) measures as medium the phosphoric acid buffer of 0.1M.
Reference example 1
In the reaction vessel with agitator, Dropping feeder, reflux and nitrogen ingress pipe, ion exchanged water 187.7 mass parts of packing into are warming up to 93 ℃ under nitrogen atmosphere gas.Then, 2 hours dropwise addition of acrylic acid 124.3 mass parts of change expense and the solution that contains Sodium Persulfate 9.8 mass parts and ion exchanged water 61.29 mass parts under this temperature.
After dripping end, under this temperature, make its reaction 6 hours, be cooled to 25 ℃ then.Then, add the aqueous sodium hydroxide solution of 30 quality %, thereby the modulation nonvolatile component is that 35 quality %, gardner viscosity are that C-D, pH are 2.61 the acrylic resin aqueous solution.
In another reaction vessel with agitator, Dropping feeder, reflux and nitrogen ingress pipe, the aforesaid propylene acid resin aqueous solution of packing into 100 mass parts are warming up to 70 ℃ under air atmosphere.Then add glycidyl methacrylate 2.4 mass parts, under this temperature, make its reaction 1 hour, aqueous sodium hydroxide solution 24.4 mass parts that add 30 quality % then, thus the modulation pH be 5.07 and number-average molecular weight be 3000 and nonvolatile component be the aqueous solution (g1) of water-soluble ethylene based polyalcohol (f1) 33.4 quality %, that have carboxyl and free-radical polymerised unsaturated double-bond.
Reference example 2
In the reaction vessel with agitator, Dropping feeder, reflux and nitrogen ingress pipe, ion exchanged water 187.7 mass parts of packing into are warming up to 93 ℃ under nitrogen atmosphere gas.Then, 2 hours dropwise addition of acrylic acid 124.3 mass parts of change expense and the solution that contains Sodium Persulfate 3.7 mass parts and ion exchanged water 61.29 mass parts.
After dripping end, under this temperature, make its reaction 6 hours, be cooled to 25 ℃ then.Then, add the aqueous sodium hydroxide solution of 30 quality %, thereby the modulation nonvolatile component is that 35 quality %, gardner viscosity are that H-I, pH are 2.57 the acrylic resin aqueous solution.
In another reaction vessel with agitator, Dropping feeder, reflux and nitrogen ingress pipe, the aforesaid propylene acid resin aqueous solution of packing into 100 mass parts are warming up to 70 ℃ under air atmosphere.Then add glycidyl methacrylate 0.9 mass parts, under this temperature, make its reaction 1 hour, aqueous sodium hydroxide solution 24.4 mass parts that add 30 quality % then, thus the modulation pH be 5.02 and number-average molecular weight be 8000 and nonvolatile component be the aqueous solution (g2) of water-soluble ethylene based polyalcohol (f2) 34.5 quality %, that have carboxyl and free-radical polymerised unsaturated double-bond.
Reference example 3
In the reaction vessel with agitator, Dropping feeder, reflux and nitrogen ingress pipe, ion exchanged water 187.7 mass parts of packing into are warming up to 93 ℃ under nitrogen atmosphere gas.The mixture of 2 hours dropwise addition of acrylic acid 121.2 mass parts of then, change expense and acrylamide 6.4 mass parts and the solution that contains Sodium Persulfate 9.8 mass parts and ion exchanged water 61.29 mass parts.
After dripping end, under this temperature, make its reaction 6 hours, be cooled to 25 ℃ then.Then, add the aqueous sodium hydroxide solution of 30 quality %, thereby the modulation nonvolatile component is that 35 quality %, gardner viscosity are that C-D, pH are 2.45 the acrylic resin aqueous solution.
In another reaction vessel with agitator, Dropping feeder, reflux and nitrogen ingress pipe, the aforesaid propylene acid resin aqueous solution of packing into 100 mass parts are warming up to 70 ℃ under air atmosphere.Then add glycidyl methacrylate 2.4 mass parts, under this temperature, make its reaction 1 hour, aqueous sodium hydroxide solution 24.4 mass parts that add 30 quality % then, thus the modulation pH be 5.33 and number-average molecular weight be 3000 and nonvolatile component be the aqueous solution (g3) of water-soluble ethylene based polyalcohol (f3) 35.3 quality %, that have carboxyl and free-radical polymerised unsaturated double-bond.
Reference example 4
In the reaction vessel with agitator, Dropping feeder, reflux and nitrogen ingress pipe, ion exchanged water 319.9 mass parts of packing into are warming up to 93 ℃ under nitrogen atmosphere gas.The mixture of 2 hours dropwise addition of acrylic acid 65.1 mass parts of then, change expense and vinylformic acid 2-hydroxyl ethyl ester 195.2 mass parts and the solution that contains Sodium Persulfate 20.2 mass parts and ion exchanged water 105 mass parts.
After dripping end, under this temperature, make its reaction 6 hours, be cooled to 25 ℃ then.Then, add the aqueous sodium hydroxide solution of 30 quality %, thereby the modulation nonvolatile component is that 35 quality %, gardner viscosity are that H, pH are 2.61 the acrylic resin aqueous solution.
In another reaction vessel with agitator, Dropping feeder, reflux and nitrogen ingress pipe, the aforesaid propylene acid resin aqueous solution of packing into 80 mass parts are warming up to 70 ℃ under air atmosphere.Then add glycidyl methacrylate 2.0 mass parts, under this temperature, make its reaction 1 hour, aqueous sodium hydroxide solution 5.2 mass parts that add 30 quality % then, thus the modulation pH be 5.22 and number-average molecular weight be 4000 and nonvolatile component be the aqueous solution (g4) of water-soluble ethylene based polyalcohol (f4) 36.2 quality %, that have carboxyl and free-radical polymerised unsaturated double-bond.
Reference example 5
In the reaction vessel with agitator, Dropping feeder, reflux and nitrogen ingress pipe, ion exchanged water 187.7 mass parts of packing into are warming up to 93 ℃ under nitrogen atmosphere gas.Then, 2 hours dropwise addition of acrylic acid 124.3 mass parts of change expense and the solution that contains Sodium Persulfate 1.5 mass parts and ion exchanged water 61.29 mass parts.
After dripping end, under this temperature, make its reaction 6 hours, be cooled to 25 ℃ then.Then, add the aqueous sodium hydroxide solution of 30 quality %, thereby the modulation nonvolatile component is that 35 quality %, gardner viscosity are that L-M, pH are 2.88 the acrylic resin aqueous solution.
In another reaction vessel with whipping appts, thermometer, reflux and nitrogen ingress pipe, the aforesaid propylene acid resin aqueous solution of packing into 100 mass parts are warming up to 70 ℃ under air atmosphere.Then add glycidyl methacrylate 0.4 mass parts, under this temperature, make its reaction 1 hour, aqueous sodium hydroxide solution 24.4 mass parts that add 30 quality % then, thus the modulation pH be 5.15 and number-average molecular weight be 20000 and nonvolatile component be the aqueous solution (g5) of water-soluble ethylene based polyalcohol (f5) 34.2 quality %, that have carboxyl and free-radical polymerised unsaturated double-bond.
Reference example 6
In 1L four-hole boiling flask with whipping appts, thermometer, reflux and nitrogen ingress pipe, add maleic anhydride 96 mass parts and ion exchanged water 50 mass parts, be warming up to 55 ℃, make the maleic anhydride dissolving.Then, to being cooled to 40 ℃ and in the pulp-like maleic anhydride that obtains, add 28 quality % ammoniacal liquor, 60.8 mass parts, under 80 ℃, make its reaction 3 hours.After the reaction, in residue 100 mass parts that ion exchanged water evaporation in making four-hole boiling flask obtains, phosphate aqueous solution 10 mass parts that add 85 quality %, in 200 ℃ oil bath, under reduced pressure make its reaction 4 hours, thus pulverous polysuccinimide that modulation has number-average molecular weight 3000.
In having another reaction vessel of whipping appts, thermometer, reflux and nitrogen ingress pipe, the sodium hydroxide 20.6 mass parts dissolved aqueous solution 75 mass parts and above-mentioned pulverous polysuccinimide 50 mass parts will be mixed, obtain the aqueous solution of polysuccinimide.Then, be warming up to 90 ℃ after, add glycidyl methacrylate 5.0 mass parts, make its reaction 1 hour, thereby the modulation number-average molecular weight be 3000 and nonvolatile component be the aqueous solution of the poly aspartic acid of 58.2 quality % with methacryloyl.
Reference example 7
In the Erlenmeyer flask of outside refrigerative 500ml, add vinylformic acid 30 mass parts, drip then and make lithium hydroxide monohydrate 8.74 mass parts dissolved lithium hydroxide aqueous solutions 81.5 mass parts, thereby 50 moles of % of the carboxyl that vinylformic acid had are neutralized.Then, add Latemul PS (alkane sulfonate Kao Corp system) 1.89 mass parts, N, N '-methylene-bisacrylamide 0.0234 mass parts and ammonium persulphate 0.05 mass parts, thus modulate acrylic acid aqueous solution (c1).
Reference example 8
In the Erlenmeyer flask of outside refrigerative 500ml, add vinylformic acid 30 mass parts, drip then and make lithium hydroxide monohydrate 8.74 mass parts dissolved lithium hydroxide aqueous solutions 81.5 mass parts, thereby with acrylic acid 50 moles of % neutralization.Then, add Praiserf A210G (phosphoric acid ester tensio-active agent, polyoxyethylene octylphenyl ether phosphoric acid, Di-ichi Kogyo Seiyaku Co., Ltd.'s system) 1.12 mass parts, N, N '-methylene-bisacrylamide 0.0234 mass parts and ammonium persulphate 0.05 mass parts, thus acrylic acid aqueous solution (e2) modulated.
Embodiment 1
In the four-hole boiling flask of the 500ml that whipping appts, thermometer, reflux and nitrogen device for blowing have been installed, add hexanaphthene 164 mass parts, Rheodol TW-O106V (polyoxyethylene sorbitol monooleate (6 moles of affixtures of oxyethane) is Kao Corp's system (HLB=10.0)) 0.82 mass parts, with 500rpm stir and on one side make its dispersion on one side.
Then, in four-hole boiling flask, carry out nitrogen displacement after, be warming up to 75 ℃, in 1 hour, drip by reference example 7 synthetic acrylic acid aqueous solution (e1).After the dropping, the aqueous solution (g1) of the above-mentioned water-soluble ethylene based polyalcohol of disposable adding (f1) (containing water-soluble ethylene based polyalcohol (f1) 8 mass parts) makes its reaction 1 hour under 70～75 ℃.After the reaction, according to azeotropic dehydration, with the 90 quality % dehydration of the water that exists in the four-hole boiling flask.Then, use the decantation separating benzene-cyclohexane, after making its predrying 3 hours under 70 ℃, under 180 ℃, carried out drying under reduced pressure 1 hour again, thus modulation core-shell high liquid-absorbing resin particle (A).The high liquid-absorbing resin particle (A) that obtains has significantly concavo-convex as shown in Fig. 1 and Fig. 2 at particle surface.
Embodiment 2
Except the aqueous solution (g2) (containing water-soluble ethylene based polyalcohol (f2) 8 mass parts) of the above-mentioned water-soluble ethylene based polyalcohol of disposable adding (f2) replaces the aqueous solution (g1) of above-mentioned water-soluble ethylene based polyalcohol (f1), use the method modulation core-shell high liquid-absorbing resin particle (B) identical with embodiment 1.The high liquid-absorbing resin particle (B) that obtains has significantly concavo-convex at particle surface.
Embodiment 3
(g3 (containing water-soluble ethylene based polyalcohol (f3) 8 mass parts) replaces the aqueous solution (g1) of above-mentioned water-soluble ethylene based polyalcohol (f1), uses the method modulation core-shell high liquid-absorbing resin particle (C) identical with embodiment 1 except the aqueous solution of the above-mentioned water-soluble ethylene based polyalcohol of disposable adding (f3).The high liquid-absorbing resin particle (C) that obtains has significantly concavo-convex at particle surface.
Embodiment 4
(g4 (containing water-soluble ethylene based polyalcohol (f4) 8 mass parts) replaces the aqueous solution (g1) of above-mentioned water-soluble ethylene based polyalcohol (f1), uses the method modulation core-shell high liquid-absorbing resin particle (D) identical with embodiment 1 except the aqueous solution of the above-mentioned water-soluble ethylene based polyalcohol of disposable adding (f4).The high liquid-absorbing resin particle (D) that obtains has significantly concavo-convex at particle surface.
Embodiment 5
In the four-hole boiling flask of the 500ml that whipping appts, thermometer, reflux and nitrogen device for blowing have been installed, add hexanaphthene 164 mass parts and Adekanol NK-4 (polyoxyethylene glycerol ester, HLB=9.5, Asahi Denka Kogyo K. K's system) 0.41 mass parts, with 500rpm stir on one side and make its dispersion on one side.Then, in four-hole boiling flask, carry out nitrogen displacement after, be warming up to 75 ℃, in 1 hour, drip by reference example 7 synthetic acrylic acid aqueous solution (e1).After the dropping, the aqueous solution (g1) of the above-mentioned water-soluble ethylene based polyalcohol of disposable adding (f1) (containing water-soluble ethylene based polyalcohol (f1) 8 mass parts) makes its reaction 1 hour under 70～75 ℃.After the reaction, according to azeotropic dehydration, with the 90 quality % dehydration of the water that exists in the four-hole boiling flask.Then, use the decantation separating benzene-cyclohexane, after making its predrying 3 hours under 70 ℃, under 180 ℃, carried out drying under reduced pressure 1 hour again, thus modulation core-shell high liquid-absorbing resin particle (E).The high liquid-absorbing resin particle (E) that obtains has significantly concavo-convex at particle surface.
Embodiment 6
Except using Nikkor TDF-8 (three polyethylene oxide alkyl ethers phosphoric acid (HLB=11.5) Nikko Chemicals Co., Ltd systems) 0.41 mass parts to replace above-mentioned Adekanol NK-4 (polyoxyethylene glycerol ester, HLB=9.5, Asahi Denka Kogyo K. K's system) beyond 0.41 mass parts, uses the method modulation core-shell high liquid-absorbing resin particle (F) identical with the foregoing description 5.The high liquid-absorbing resin particle (F) that obtains has significantly concavo-convex at particle surface.
Embodiment 7
In the four-hole boiling flask of the 500ml that whipping appts, thermometer, reflux and nitrogen device for blowing have been installed, add hexanaphthene 164 mass parts and Rheodol SP-S10V (Kao Corp's system, sorbitan monostearate) 0.2 mass parts, with 500rpm stir on one side and make its dispersion on one side.Then, in four-hole boiling flask, carry out nitrogen displacement after, be warming up to 75 ℃, in 1 hour, drip by reference example 8 synthetic acrylic acid aqueous solution (e2).After dripping end, the aqueous solution (g1) of the above-mentioned water-soluble ethylene based polyalcohol of disposable adding (f1) (containing water-soluble ethylene based polyalcohol (f1) 8 mass parts) makes its reaction 1 hour under 70～75 ℃.After the reaction, according to azeotropic dehydration, with the 90 quality % dehydration of the water that exists in the four-hole boiling flask.Then, use the decantation separating benzene-cyclohexane, after making its predrying 3 hours under 70 ℃, under 180 ℃, carried out drying under reduced pressure 1 hour again, thus modulation core-shell high liquid-absorbing resin particle (G).The high liquid-absorbing resin particle (G) that obtains has significantly concavo-convex at particle surface.
Comparative example 1
In the four-hole boiling flask of the 500ml that whipping appts, thermometer, reflux and nitrogen device for blowing have been installed, add hexanaphthene 164 mass parts and Rheodol SP-S10V 0.2 mass parts, with 500rpm stir and on one side make its dispersion on one side.Then, in four-hole boiling flask, carry out nitrogen displacement after, be warming up to 75 ℃, in 1 hour, drip by reference example 8 synthetic acrylic acid aqueous solution (e2), after making its predrying 3 hours under 70～75 ℃, under 180 ℃, carried out drying under reduced pressure 1 hour again, thus modulation high liquid-absorbing resin particle (H).
Comparative example 2
The aqueous solution (containing the poly aspartic acid that 8 mass parts have methacryloyl) of the poly aspartic acid with methacryloyl that is obtained by reference example 6 except disposable adding replaces the aqueous solution (g1) of above-mentioned water-soluble ethylene based polyalcohol (f1), uses the manufacture method modulation high liquid-absorbing resin particle (I) identical with embodiment 1.
Comparative example 3
Except the vinylformic acid of disposable adding 8 mass parts replaces the aqueous solution (g1) of above-mentioned water-soluble ethylene based polyalcohol (f1), use the manufacture method modulation high liquid-absorbing resin particle (J) identical with embodiment 1.
Comparative example 4
In the four-hole boiling flask of the 500ml that whipping appts, thermometer, reflux and nitrogen device for blowing have been installed, add hexanaphthene 164 mass parts and Rheodol TW-O106V (polyoxyethylene sorbitol monooleate (oxyethane; 6 moles of affixtures) (HLB=10.0) Kao Corp's system) 0.82 mass parts, with 500rpm stir and on one side make its dispersion on one side.
Then, in four-hole boiling flask, carry out nitrogen displacement after, be warming up to 75 ℃, in 1 hour, drip by reference example 7 synthetic acrylic acid aqueous solution (e1).After the dropping, the aqueous solution (g5) of the above-mentioned water-soluble ethylene based polyalcohol of disposable adding (f5) (containing water-soluble ethylene based polyalcohol (f5) 8 mass parts), the result is because viscosity rises, and stirring velocity becomes about 330rpm.Then under 70～75 ℃, make its reaction 1 hour, then according to azeotropic dehydration, with the 90 quality % dehydration of the water that exists in the four-hole boiling flask.Then, use the decantation separating benzene-cyclohexane, after making its predrying 3 hours under 70 ℃, under 180 ℃, carried out drying under reduced pressure 1 hour again, thus modulation high liquid-absorbing resin particle (K).
[table 1]
Abbreviation in the following his-and-hers watches 1 describes.
AA: vinylformic acid
AM: acrylamide
HEA: vinylformic acid 2-hydroxyl ethyl ester
Pasp: by the poly aspartic acid with methacryloyl of reference example 6 acquisitions
Prove that by The above results excellent effect of the present invention is obvious.
Utilizability on the industry
The present invention goes for being conducive to the manufacture method various fields, high liquid-absorbing resin particle headed by medical treatment, the health field
Claims (3)
1. the manufacture method of core-shell high liquid-absorbing resin particle, it is characterized in that having (1) in the hydrophobic organic solvent that contains nonionic surfactant (b) (a), make the aqueous solution (e) that contains (methyl) vinylformic acid, linking agent (c) and anionic surfactant (d) carry out suspension polymerization and form the particle core first operation and
(2) in the suspension that obtains by described first operation, make to contain and have carboxyl and polymerizability unsaturated double-bond, and the aqueous solution (g) with water-soluble ethylene based polyalcohol (f) of 500～10000 number-average molecular weights carries out suspension polymerization and forms second operation of the shell portion that covers above-mentioned particle core
Wherein, described nonionic surfactant (b) has 4～13 HLB, and described anionic surfactant (d) is following material with general formula (I) expression,
R’-SO
3M (I)
R ' expression in the general formula (I) has the alkenyl of carbonatoms 8～30 or has the hydroxyalkyl of carbonatoms 8～24; M represents basic metal, quaternary ammonium salt or quaternary ammonium.
2. the manufacture method of the core-shell high liquid-absorbing resin particle of claim 1 record, wherein, described water-soluble ethylene based polyalcohol (f) is the polyacrylic acid with polymerizability unsaturated double-bond.
3. the manufacture method of the core-shell high liquid-absorbing resin particle of claim 1 record, wherein, described nonionic surfactant (b) is at least a of the phosphotriester that is selected from the polyoxyalkylene sorbitan fatty(acid)ester with 9～11HLB, the polyoxyalkylene glycerol fatty acid ester with 9～10HLB and has 7～13HLB.
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2004019757 | 2004-01-28 | ||
| JP019757/2004 | 2004-01-28 |
Publications (2)
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| CN1898285A CN1898285A (en) | 2007-01-17 |
| CN100422230C true CN100422230C (en) | 2008-10-01 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNB2005800013180A Expired - Fee Related CN100422230C (en) | 2004-01-28 | 2005-01-21 | Method for producing core-shell high liquid-absorbing resin particle |
Country Status (6)
| Country | Link |
|---|---|
| US (1) | US8013049B2 (en) |
| EP (1) | EP1669381B1 (en) |
| CN (1) | CN100422230C (en) |
| DE (1) | DE602005024099D1 (en) |
| TW (1) | TW200536864A (en) |
| WO (1) | WO2005073263A1 (en) |
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| BRPI0507428B8 (en) * | 2004-02-05 | 2021-07-27 | Nippon Catalytic Chem Ind | particulate agent for water absorption, production method and absorbent article |
| SE0502485L (en) * | 2005-11-09 | 2007-05-10 | Peter Viberg | particles |
| CN104024281B (en) | 2012-02-29 | 2015-11-25 | 住友精化株式会社 | The manufacture method of water-absorbent besin particles |
| KR101513146B1 (en) | 2013-09-30 | 2015-04-17 | 주식회사 엘지화학 | Preparation method for super absorbent polymer |
| KR20180118620A (en) | 2016-03-02 | 2018-10-31 | 스미토모 세이카 가부시키가이샤 | Method for producing absorbent resin particles |
Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2003033652A (en) * | 2001-07-26 | 2003-02-04 | Dainippon Ink & Chem Inc | Water absorptive material and blood absorbing article using the same |
| JP2003206324A (en) * | 2002-01-11 | 2003-07-22 | Dainippon Ink & Chem Inc | Water absorbing material |
| JP2003245544A (en) * | 2002-02-21 | 2003-09-02 | Dainippon Ink & Chem Inc | Water absorptive material |
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| BE755471A (en) * | 1969-08-29 | 1971-02-01 | Sumitomo Chemical Co | DETERGENT COMPOSITION OF OLEFINE SULPHONATE |
| EP0516925B1 (en) | 1991-03-19 | 1998-05-06 | The Dow Chemical Company | Wrinkled absorbent particles of high effective surface area having fast absorption rate |
| WO1993019099A1 (en) | 1991-03-19 | 1993-09-30 | The Dow Chemical Company | Wrinkled absorbent particles of high effective surface area having fast absorption rate |
| EP0624606B2 (en) * | 1993-05-14 | 2003-08-27 | Mitsui Takeda Chemicals, Inc. | Core-shell polymer and plastisol therefrom |
| JP2001031704A (en) | 1999-07-19 | 2001-02-06 | Mitsubishi Chemicals Corp | Manufacture of highly water absorptive resin |
| JP4550256B2 (en) | 1999-11-19 | 2010-09-22 | 三洋化成工業株式会社 | Manufacturing method of water absorbent resin |
| KR100579940B1 (en) * | 2001-04-16 | 2006-05-15 | 스미토모 세이카 가부시키가이샤 | Water-absorbing resin suitable for absorbing viscous liquid containing high-molecular compound, and absorbent and absorbent article each comprising the same |
| JP3640921B2 (en) * | 2001-12-28 | 2005-04-20 | クラリアントポリマー株式会社 | Synthetic resin emulsion, easily water-swellable pressure-sensitive adhesive composition comprising the same, and method for producing synthetic resin emulsion |
| JP2005047977A (en) | 2003-07-30 | 2005-02-24 | Dainippon Ink & Chem Inc | Method for producing absorbing resin |
-
2005
- 2005-01-21 WO PCT/JP2005/000750 patent/WO2005073263A1/en active Application Filing
- 2005-01-21 CN CNB2005800013180A patent/CN100422230C/en not_active Expired - Fee Related
- 2005-01-21 US US10/576,362 patent/US8013049B2/en not_active Expired - Fee Related
- 2005-01-21 EP EP05703971A patent/EP1669381B1/en not_active Expired - Fee Related
- 2005-01-21 DE DE602005024099T patent/DE602005024099D1/en active Active
- 2005-01-25 TW TW094102143A patent/TW200536864A/en unknown
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2003033652A (en) * | 2001-07-26 | 2003-02-04 | Dainippon Ink & Chem Inc | Water absorptive material and blood absorbing article using the same |
| JP2003206324A (en) * | 2002-01-11 | 2003-07-22 | Dainippon Ink & Chem Inc | Water absorbing material |
| JP2003245544A (en) * | 2002-02-21 | 2003-09-02 | Dainippon Ink & Chem Inc | Water absorptive material |
Also Published As
| Publication number | Publication date |
|---|---|
| WO2005073263A1 (en) | 2005-08-11 |
| US20070276061A1 (en) | 2007-11-29 |
| EP1669381A1 (en) | 2006-06-14 |
| EP1669381A4 (en) | 2008-11-19 |
| EP1669381B1 (en) | 2010-10-13 |
| TW200536864A (en) | 2005-11-16 |
| DE602005024099D1 (en) | 2010-11-25 |
| US8013049B2 (en) | 2011-09-06 |
| CN1898285A (en) | 2007-01-17 |
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